Note: Descriptions are shown in the official language in which they were submitted.
;3~
l ~ ~16
Fluid ptrrification
~his invention relate~ to fluid purification and in
particular to the removal of trace impurities from fluids to be
treated in highly sensiti~e systems such as catalysis.
~s described in our ~S pate~t 4177252 in relatio~t to
the effect of compounds of halogens or s~lphttr on metallic cop-
per shift cataly~ts, the chemical reactions by which such trace
impurities exert their undesired action are very rapid and occttr
mainly ~t external geometric surfaces. Consequently it was pro-
posed to carry out the shif-t reaction in a fixed catalyst bed
having an inlet zone in which the voltmne-to-surface ratio of the
catalyst pieceæ is less than in an outlet zone. This waæ to be
provided for by using in the i~let zone catalyst pieces that were
smaller than in the outlet zone or were formed with indentations
or protrusions or lobe~.
We have ~ow realised that the inlet zo~e shapes dis-
closed in ~S 4177252 provide a relatively small increase in geo-
metric surface u~less a substantially inoreased pressure drop càn
be tolerated9 and that this constraint can be evaded by use of a
suitably struotured absorbent material.
~ ccording to the invention a process for removing trace
impurities f~om a flowing fluid by means of a solid absorbent is
characterised in that the absor~ent is in a physioal form ha~ing
a geometric surface area per unit pressure drop (hereinafter
referred to as'~ ~ value") of at least 0.1 expressed in S.I units.
For the purposes of the invention the pressure drop is
~ .,
2 ~ 31643
no~m31i3ed by application of the following expres~ion to the pres-
sure drop P as measured:
~ormali3ed pressure drop _
where
A P iæ in Pa
u is the fluid velocity in m/sec (This is calculated
as if the absorbent bed were empty)
i8 the fluid d~næity in kg/m3
~ is the length of the bed in m.
~he geometric surface area is to be distinguished from
the internal surface area: since the rate of trace impurity
absorption is determined by dif~usion through a surface film of
fluid and receives a negligibly small contribution from diffusion
into pores, the internal surface area of the absorbent îs not in-
volved. The geometric su~face area is, for the purposes of the
invention e~pressed per unit volume of a ve sel filled with the
absorbent. Using units consistent with the pressure drop uni-ts
its dimensions are m2 m 3, that is, m 1. Consequently the geo-
metric surface area per unit presæure drop is dimensionless.
Other self-consistent dimen3ion3 could be uAed, if de-
sired, and the limit specified would differ correspondingly.
Variously shaped absorbents can be uæed. In general
the shapes i~clude flattened members of thickness under about
2 mm and æ e non-nesting: saddles are an exampleO In a~ espec-
ially use~ul process the absorbent is in the form of at least
one structure havLng at least one through~passage.
~ he effect of the through passage or passages is to
decrease the pre~sure drop for a given geometric surface æ ea.
~aking a ra~dom_packed bed of 3.6 x 5.4 mm squat cylindrical pel-
lets as standard, these have a G~ value of o.o6, but the absor-
bent ~tructures u~ed in the process have a G~ value at least 1.7
time~, preferably at least 3 times as great (0.2 or more)O ~his
improvement is readily attainable using cylindriGal rings~ ~ more
substantial Lmprovement (at leaæt 6-fold, to 0.4 ~ 0.7) can be
obtained by using rings fox~ed with internal webs. The process
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preferably employs an absorbent in the form of random-packed coils
or sm~ll horeycomb pieces havLng a G~ value of at least o.6, that
is at least 10 times as great as the above standard. In a fuFther
preferred form of the process the absorbent is in the.form of a
monolithic structure, in which event a G~ value at least 20 and
preferably in the range 30 - 150 times the above standard is pro~
vided (that is, at least 1.2 especi~lly 1.8 to 9.0)~ ~bsorbent
shapes can, of course, be used in which less than such possible
high surface areas are provided. A usefully high G/P value
10 can be obtained using foraminate sheet metal, for
example gauze or expanded metal.
Owing to the low or very low pressure drop, the process
can be carried out in long beds, having for example a length at
least equ 1 to and in the r~4ge 1 - 10 times, its diameter. As
a result fluid flow velocities can be high enough to mi~imise
film diffusion limitation and thus ensure effective removal of
impurities present in extremoly small trace quantities.
The absorbent can be in the fo~m of a cartridge readily
insertable into and removable from a reactor or even from a
position in a pipe or a widened region in a pipe. If the absor-
bent i9 random-packed the cartridge includes a perforated container.
If it is in sheet foxm, the sheets can be held together by tie rods.
~mong the structures especially suitable are the following:
1. rinB~ of diameter in the range 5 - 20 mm (exte~al),
length 5 - 20 mm and thickness 0.5 - 10 mm when made
of ceramic or down to 0.03 mm when made of metal or
alloy;
2. webbed rings of the same diameter and length as the
rin6s but with maximum thickness 5 mm~ Similarly
incompletely bridged rings such as "PALL" rings c n
be used;
(For 1 or 2 split or spiralled rings can be used)O
coils of wire or strip of thickness in the same ranges
as for webbed rings, again depending on whether they
are made of ceramic or metal. The outside dimensions
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are ty~ically in the range 5 - 20 mm in diameter and
10 - 100 mm in length;
4. small honeycombs having the same diame-ter and hei~ht
ranges as the rings and ha~ing an open area of at
least 3~/0, especially in the range 50 - 90%. Iypic-
ally such honeycombs have 10 - 100 passages per cm2;
5. monoliths having an open area of a-t least 30/0, espec-
ially in -the range 50 - 9~/. In a flow process a
single monolith occupying the cross-sectional area
of the vessel can be used or, more conveniently, a
set of monol~^th units can be disposed side by side.
The effects of a monolîth can be obtained by stacking
sheets parallel to the direction of fluid flow ox (with
suitable perforations) transversely or anglad to that
directionO ~ particularly suitable monolithic--type
structure is described in our co-pending 3uropean
applioztion 80302945 (published undex Serial ~o.
25308): this haæ through-flow passages a~gled to -the
general direction of fluid flow and is spaced from the
w lls of its containing vessel so as to cause the fluid
to flow alter~atingly through the passages and through
the space between the structure a~d the walls. Our
application describes various structures providing this
flowpath, for example slant-cell honeycombæ of ceramic
or metal, stacked profiled plates and co-operating per-
forated plates such as expanded metal sheets~ ~he
flo~-path within the structure can be in a secantial or,
in an annular~section vessel, can be in a radial com-
ponent or direction superimposed on the general flow
directionO As a further alternative the monolith may
be constituted by perforated (such as expana~d metal)
sheets not aligned to such through-passages;
6v gau es and other woven or non-woven masses. ~hese pro-
vide a ve~y high surface area per unit of pressure
drop, but are less generally applicable because they
~3æ
5 ~ 31643
lack rigidity. They can be used in r~tdsm-pack or
monolithic form;
7. open-cell fo~ms. ~hese likewise calt be used iIt random-
pack or monolithic form.
~he above mentioned monoliths, such as are provided by
expanded metal, in which parallel bu-t interrupted flow-paths are
present, are especially preferr0d, since they suffer from film
diffusion limitation no more than a random-packed bed, yet affoxd
a m~tch lower pressure drop, because "form-drag" is vexy much less.
0 it i9 within the scope of the ~tvention -to introduce turbt~ence by
providing deflection of flow, as in non-aligned expanded metal,
especially when film diffusion limitation is serious. This increases
pressure drop but an increase by a factor of 4 is sufficient.
The structures can be composed of a~y material that will
withstand the conditions of useO Ceramics such as alumina, alumino-
silicate, cordierite and spinels and also glasses and glass-cëramics
are of ge~eral applicabilityO Metals and alloys, especially iron
alloys containi~g one or more of aluminium9 ohromium or silicon, as
described in our ¢o-pendi~g European application 80301982 published
under Serial ~o. 21736, are especially ~uitable, beoause they can
be formed into structures o~ ve~y high surface area per unit pres-
sure drop and can be readily coated.
~mong the absorbents that are especially useful are
A. chemically-active compounds, for example
oxides of Cu, Zn, Mn or Fe, for removing E2S
oxides more basic than ZnO, for removing halogen hydracid
(e~am~les are hydroxides, aluminates and carbonates or
alkali metals)O
cataly~ts, e~pecially of the type from which the trace
impurities are to be excluded.
. highly porous absorbents, for example
alumina, for remo~ing water
ions exchange resins, for removing ions
molecular sieves, such as carbon or crystalline ~eolites,
for removing relatively in~olatile gases such as normally
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liquid compounds, gaseous hYdrocarbons, vi~yl chloride,
nitrogen oxides, ammonia, C02, C0 and nitrogen.
Such absorbents can a & ere direc-tly to the struc-ture or
to an intervening coating such as of alumina, chromia ox silica.
Such an intervening coa-ting can be the product of superfioially
oxidising a metallic constituent of the structure and/or of applic-
ation as a washcoat or a soluble decomposable compoundO
In an important embodiment the invention provides a pro-
cess Por reacting carbon monoxide with ste~m to give carbon dioxide
and hydrogen over a coppar-containing shift catalyst9 in which
poiso~ing of the catalyst by traces of compounds of sulphur or
chlorine is i~hibited by subjecting the reactants to the process
of the i~vention; the absorbent can comprise for example a compound
more basic than zinc oxide, as broadly disclosed for example in our
~S patents 3922337 and 3943226, or can be a coating on a support
of the copper-containing catalyst or a catalyst modified to con-
tain less copper, as described in our ~S patent 4177252.
In another important embodiment the invention provides
a process of purifying from halogen compounds a hydrocarbon feed-
stock, especially a naphtha or LPG to be subjected to catalyticreaction with staam at u~der 600C to give a methane-cont~;n;ng
gasO ~hi8 purificatio~ process uses as absorbent an oxide more
basic than zinc oxide and preferably follows a catalytic h~dro-
genation step in which at least organic sulphur is converted to
H2S and an ~2S removal step. The effect of the catalytic hydro-
treatment is to con~ert organic halogen to halogen hydracidO
~XA~IE
Each of a series of absorbents or structures capable of
supporting absorbent was set up in a catalyst bed 275 mm deep,
91 mm in diameter, and subjected to an air flow of 20 m3h 1 at
20C. ~he pressure difference ~ P between the inlet and outlet
air was measured in Pa and normalised as described aboveO (~he
gas density was taken as 1.2, assu~ing atmospheric pressure, and
- the gas velocity 0.85 m/sec). It was al~o expressed relative
to 3.6 x 504 mm squat cylindrical pellets taken as standard tlOO)o
863æ
7 B 31643
~he geometric surfaoe of the samples was calculated from the
weight of the sample filling the catalyst bed, the a~erage
weight of each piece and the dimensions of eaoh pieceO
In addition, the calculated pressure drop for a stack
of randomly-oriented sheets of expanded metal of thiolmess 004 mm,
with rectang~lar apertures 3D mm long, strand width 5 mm and
strand pitch 3 mm. This was chosen because its area is about the
same as cylindrical pellets: clearly much finer grades could be
usedO
8 ~ 316~3;
~I,E
Absorbent piece 3hape Surface ~ area per
and dimensions, mm area Pa Rela- m~l unit
m~l tive PdrropSUre
_ _ . __. _.
Cylinders d h
3-45 3-65 1140 1913115 15900 0.072
5-4 ~.6 860 1667100 13900 00062
8.7 6.7 520 765 46 6~oo 0.081
8.7 13.0 380 47 28 3900 0.097
Spheres 6.4 520 736 44 6100 0.085
(~he abov ,_are compar ~ not acc r in~ to the inven-
Rings OD ID h
8.4 6.1 7-5 620 343 21 2858 0.218
15.5 7-9 6.2 37 186 11 1550 0.239
15.411.2 L5-7 260 118 7 990 0.262
16.3 9-5 L7~3 260 98 6 810 0.32
Rings with 7 OD ~E h
radiaL webs17-3 2 8.5 480 137 8 1140 0.421
Hings with
5 radiaL webs 17.0 2 17-3 44 78 5 650 o.677
SmaLl honey-
combs (metal)
of pen 17.00.05 15-51600 177 11 1475 1.08
area about
Ceramic mono- - o.3
lith : 36 equi-
later~L _ o~3 _ 2500123 7 1025 2-44
tr~angles per
Coils of wire 6.4 o.5 12.7 1200157 9 1308 0.92
___ ___ _ . . , .
Expanded
metaL (cal- _ 0.4 _ 420 120 7.2 1000 0.42
cuLated values~
__ ~ ___ ~ - __ _ ,
~ote: d = diameter, h = height, OD = outside diameter,
ID = inside diameter, ~E = thickness
PA ~ C ~ P
30 ~ovember 1981
